Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of p-Cresol (1) - Liquid mixture 1 |
---|---|
298.15 | 0.0569 |
313.15 | 0.1025 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
Temperature, K - Liquid mixture 2 | Mole fraction of p-Cresol (1) - Liquid mixture 2 |
---|---|
298.15 | 0.4736 |
313.15 | 0.4350 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Heptane (2) - Liquid mixture 1 |
---|---|
298.15 | 0.9229 |
313.15 | 0.8517 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
Temperature, K - Liquid mixture 2 | Mole fraction of Heptane (2) - Liquid mixture 2 |
---|---|
298.15 | 0.1220 |
313.15 | 0.1523 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of Heptane (2) - Liquid mixture 1 | Mole fraction of p-Cresol (1) - Liquid mixture 1 |
298.15 | 0.0000 | 0.4814 |
298.15 | 0.0207 | 0.4850 |
298.15 | 0.0317 | 0.4888 |
298.15 | 0.0347 | 0.4857 |
298.15 | 0.0509 | 0.4853 |
298.15 | 0.0740 | 0.4796 |
298.15 | 0.0791 | 0.4831 |
298.15 | 0.0968 | 0.4781 |
298.15 | 0.1141 | 0.4749 |
298.15 | 0.1410 | 0.5076 |
298.15 | 0.1482 | 0.5121 |
298.15 | 0.1812 | 0.5350 |
298.15 | 0.1873 | 0.5378 |
298.15 | 0.1902 | 0.5390 |
298.15 | 0.2182 | 0.5456 |
298.15 | 0.2333 | 0.5485 |
298.15 | 0.2695 | 0.5408 |
298.15 | 0.2796 | 0.5340 |
298.15 | 0.3146 | 0.5224 |
298.15 | 0.3338 | 0.5092 |
298.15 | 0.3830 | 0.4812 |
298.15 | 0.4027 | 0.4660 |
298.15 | 0.4685 | 0.4193 |
298.15 | 0.5387 | 0.3667 |
298.15 | 0.6182 | 0.3044 |
298.15 | 0.6979 | 0.2405 |
298.15 | 0.7754 | 0.1777 |
298.15 | 0.8151 | 0.1500 |
298.15 | 0.8577 | 0.1140 |
298.15 | 0.9364 | 0.0500 |
298.15 | 0.0347 | 0.4905 |
323.15 | 0.0000 | 0.4380 |
323.15 | 0.0623 | 0.4560 |
323.15 | 0.0872 | 0.4548 |
323.15 | 0.1263 | 0.4475 |
323.15 | 0.1594 | 0.4392 |
323.15 | 0.1754 | 0.4390 |
323.15 | 0.1956 | 0.4455 |
323.15 | 0.2108 | 0.4584 |
323.15 | 0.2220 | 0.4512 |
323.15 | 0.2488 | 0.4497 |
323.15 | 0.2615 | 0.4529 |
323.15 | 0.2925 | 0.4450 |
323.15 | 0.3079 | 0.4399 |
323.15 | 0.3419 | 0.4122 |
323.15 | 0.3663 | 0.4115 |
323.15 | 0.3840 | 0.4033 |
323.15 | 0.4219 | 0.3860 |
323.15 | 0.4577 | 0.3604 |
323.15 | 0.5142 | 0.3338 |
323.15 | 0.5360 | 0.3123 |
323.15 | 0.6320 | 0.2518 |
323.15 | 0.6848 | 0.2195 |
323.15 | 0.7188 | 0.1920 |
323.15 | 0.7965 | 0.1395 |
323.15 | 0.8749 | 0.0928 |
323.15 | 0.9296 | 0.0582 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of p-Cresol (1) - Liquid mixture 1 |
---|---|
298.15 | 0.0569 |
313.15 | 0.1025 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
Temperature, K - Liquid mixture 2 | Mole fraction of p-Cresol (1) - Liquid mixture 2 |
---|---|
298.15 | 0.4736 |
313.15 | 0.4350 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Heptane (2) - Liquid mixture 1 |
---|---|
298.15 | 0.9229 |
313.15 | 0.8517 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
Temperature, K - Liquid mixture 2 | Mole fraction of Heptane (2) - Liquid mixture 2 |
---|---|
298.15 | 0.1220 |
313.15 | 0.1523 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of Heptane (2) - Liquid mixture 1 | Mole fraction of p-Cresol (1) - Liquid mixture 1 |
298.15 | 0.0000 | 0.4814 |
298.15 | 0.0207 | 0.4850 |
298.15 | 0.0317 | 0.4888 |
298.15 | 0.0347 | 0.4857 |
298.15 | 0.0509 | 0.4853 |
298.15 | 0.0740 | 0.4796 |
298.15 | 0.0791 | 0.4831 |
298.15 | 0.0968 | 0.4781 |
298.15 | 0.1141 | 0.4749 |
298.15 | 0.1410 | 0.5076 |
298.15 | 0.1482 | 0.5121 |
298.15 | 0.1812 | 0.5350 |
298.15 | 0.1873 | 0.5378 |
298.15 | 0.1902 | 0.5390 |
298.15 | 0.2182 | 0.5456 |
298.15 | 0.2333 | 0.5485 |
298.15 | 0.2695 | 0.5408 |
298.15 | 0.2796 | 0.5340 |
298.15 | 0.3146 | 0.5224 |
298.15 | 0.3338 | 0.5092 |
298.15 | 0.3830 | 0.4812 |
298.15 | 0.4027 | 0.4660 |
298.15 | 0.4685 | 0.4193 |
298.15 | 0.5387 | 0.3667 |
298.15 | 0.6182 | 0.3044 |
298.15 | 0.6979 | 0.2405 |
298.15 | 0.7754 | 0.1777 |
298.15 | 0.8151 | 0.1500 |
298.15 | 0.8577 | 0.1140 |
298.15 | 0.9364 | 0.0500 |
298.15 | 0.0347 | 0.4905 |
323.15 | 0.0000 | 0.4380 |
323.15 | 0.0623 | 0.4560 |
323.15 | 0.0872 | 0.4548 |
323.15 | 0.1263 | 0.4475 |
323.15 | 0.1594 | 0.4392 |
323.15 | 0.1754 | 0.4390 |
323.15 | 0.1956 | 0.4455 |
323.15 | 0.2108 | 0.4584 |
323.15 | 0.2220 | 0.4512 |
323.15 | 0.2488 | 0.4497 |
323.15 | 0.2615 | 0.4529 |
323.15 | 0.2925 | 0.4450 |
323.15 | 0.3079 | 0.4399 |
323.15 | 0.3419 | 0.4122 |
323.15 | 0.3663 | 0.4115 |
323.15 | 0.3840 | 0.4033 |
323.15 | 0.4219 | 0.3860 |
323.15 | 0.4577 | 0.3604 |
323.15 | 0.5142 | 0.3338 |
323.15 | 0.5360 | 0.3123 |
323.15 | 0.6320 | 0.2518 |
323.15 | 0.6848 | 0.2195 |
323.15 | 0.7188 | 0.1920 |
323.15 | 0.7965 | 0.1395 |
323.15 | 0.8749 | 0.0928 |
323.15 | 0.9296 | 0.0582 |